JP2002028635A - Gas-liquid separator in ozone water producer - Google Patents

Gas-liquid separator in ozone water producer

Info

Publication number
JP2002028635A
JP2002028635A JP2000217887A JP2000217887A JP2002028635A JP 2002028635 A JP2002028635 A JP 2002028635A JP 2000217887 A JP2000217887 A JP 2000217887A JP 2000217887 A JP2000217887 A JP 2000217887A JP 2002028635 A JP2002028635 A JP 2002028635A
Authority
JP
Japan
Prior art keywords
gas
ozone water
ozone
inner cylinder
water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2000217887A
Other languages
Japanese (ja)
Inventor
Toshiya Ishida
敏也 石田
Kazuaki Baba
和昭 馬場
Kiyoto Fujii
清人 藤井
Naoki Tohana
直樹 戸花
Tomoaki Sakata
知昭 坂田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Max Co Ltd
Original Assignee
Max Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Max Co Ltd filed Critical Max Co Ltd
Priority to JP2000217887A priority Critical patent/JP2002028635A/en
Publication of JP2002028635A publication Critical patent/JP2002028635A/en
Pending legal-status Critical Current

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  • Oxygen, Ozone, And Oxides In General (AREA)
  • Degasification And Air Bubble Elimination (AREA)
  • Physical Water Treatments (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a gas-liquid separator capable of miniaturizing an ozone water tank 5 and efficiently separating ozone gas and ozone water. SOLUTION: In an ozone water producer provided with the ozone water tank 5 for storing gaseous ozone generated by an ozone generator in a state dissolved into water, an inflow port 8 of gas-liquid mixed water of both water and gaseous ozone is formed at the upper part of the ozone water tank 5 and also a discharge port 9 is formed at the lower part, and an inner cylinder 10 closed at the upper end with an upper cap 11 is arranged at the inside of the ozone water tank 5, and gas-liquid mixed water is allowed to flow into the upper part of the inner cylinder 10 while it swirls, and an exhaust hole of gaseous ozone is formed at the upper cap 11 of the inner cylinder 10 and also discharge holes of ozone water in the inner cylinder 10 are formed at the lower end of the inner cylinder 10 in contact with the bottom of the outer cylinder.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】本発明はオゾン水生成器におけるオゾンガ
スとオゾン水とを分離する気液分離装置に関する。
The present invention relates to a gas-liquid separator for separating ozone gas and ozone water in an ozone water generator.

【0002】[0002]

【従来技術】一般に、オゾン水生成器は水道水等にオゾ
ンガスを溶解させてオゾン水を生成するもので、オゾン
水生成器から排出されたオゾン水は、病院の医療器具や
野菜、果物等の生鮮食品や厨房の備品、食器などの洗
浄、消毒、消臭等の用途に使用される。オゾン水は消
毒、消臭等には有効であるが、オゾンガスは健康上好ま
しくないと言われているので、水道水等にオゾンガスを
溶解させた後、溶解せずに余った余剰オゾンガスとオゾ
ン水とは完全に分離してオゾン水のみを排出する必要が
ある。
2. Description of the Related Art Generally, an ozone water generator dissolves ozone gas in tap water or the like to generate ozone water, and ozone water discharged from the ozone water generator is used for hospital medical equipment, vegetables, fruits and the like. It is used for washing, disinfecting, deodorizing fresh foods, kitchen equipment, tableware, etc. Although ozone water is effective for disinfection and deodorization, it is said that ozone gas is not desirable for health, so after dissolving ozone gas in tap water etc., excess ozone gas and ozone water And only ozone water needs to be discharged.

【0003】そのため、オゾン水生成器には図10に示
すようなオゾン水タンク20が設けられ、このオゾン水
タンク20にオゾンガスと水との気液混合水が貯留さ
れ、ここでオゾンガスとオゾン水とに分離した後、オゾ
ンガスを分解処理して大気に放出し、オゾン水のみが排
出されるように構成されている。そのため、オゾン水タ
ンクには水流案内筒21が形成され、内部に流入したオ
ゾンガスとオゾン水の気液混合水が渦を巻いて下方に移
動して吐出口22に移動するように構成されている。オ
ゾン水の渦巻の内側の圧力は低くなるので、軽いオゾン
ガスの気泡23は渦の内側に入り込み、やがてその浮力
により上昇して分解装置側に移動する。
For this purpose, the ozone water generator is provided with an ozone water tank 20 as shown in FIG. 10, and the ozone water tank 20 stores a gas-liquid mixture of ozone gas and water. Then, the ozone gas is decomposed and released into the atmosphere, and only ozone water is discharged. Therefore, a water flow guide tube 21 is formed in the ozone water tank, and the ozone gas and the ozone water gas-liquid mixed water flowing inside are swirled and moved downward to move to the discharge port 22. . Since the pressure inside the ozone water swirl decreases, the light ozone gas bubbles 23 enter the inside of the swirl, and eventually rise due to their buoyancy and move to the decomposition device side.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、このよ
うな自然分離方式の気液分離装置を採用する場合、オゾ
ン水タンクには高さが必要となる。その理由は、タンク
が低いと、気泡は水流に巻き込まれて吐出口22に引き
込まれてしまいやすいからである。オゾン水タンクが大
型であれば、比較的効率的に気液の分離を行なうことが
できるが、オゾン水タンクをコンパクトにしようとする
場合、オゾンガスの泡は上昇する前にオゾン水の流れに
巻き込まれて吐出口22から排出されてしまいやすい。
However, when such a natural-separation type gas-liquid separator is used, the ozone water tank needs to be high. The reason for this is that if the tank is low, the air bubbles are likely to be caught in the water stream and drawn into the discharge port 22. If the ozone water tank is large, gas-liquid separation can be performed relatively efficiently, but when trying to make the ozone water tank compact, the ozone gas bubbles are caught in the flow of ozone water before rising. And is easily discharged from the discharge port 22.

【0005】本発明は上記問題点を解消し、オゾン水タ
ンクを小型にすると同時に、オゾンガスとオゾン水とを
効率よく分離することができるオゾン水生成器における
気液分離装置を提供することをその課題とする。
It is an object of the present invention to provide a gas-liquid separator for an ozone water generator which can solve the above-mentioned problems and reduce the size of an ozone water tank and efficiently separate ozone gas and ozone water. Make it an issue.

【0006】[0006]

【課題を解決するための手段】前記課題を解決するた
め、本発明に係るオゾン水生成器における気液分離装置
は、オゾン発生体で発生させたオゾンガスを水に溶かし
た状態で貯留するオゾン水タンクを備えたオゾン水生成
器において、上記オゾン水タンクの上部には水とオゾン
ガスの気液混合水の流入口を、下部には吐出口を形成す
るとともに、オゾン水タンクの内側に上端を上蓋で閉じ
た内筒を配置し、上記流入口から内筒の上部に気液混合
水が渦を巻いて流入するようになし、内筒の上蓋にはオ
ゾンガスの排気孔を形成するとともに、外筒の底部に当
接した内筒の下端には内筒内のオゾン水の排出孔を形成
したことを特徴とする。
In order to solve the above-mentioned problems, a gas-liquid separation device in an ozone water generator according to the present invention comprises an ozone water storing ozone gas generated by an ozone generator in a state of being dissolved in water. In an ozone water generator equipped with a tank, an inlet for gas-liquid mixture of water and ozone gas is formed at an upper part of the ozone water tank, and a discharge port is formed at a lower part. A gas-liquid mixture is swirled into the upper part of the inner cylinder from the inflow port and flows into the upper part of the inner cylinder. An exhaust hole for ozone gas is formed in the upper lid of the inner cylinder. A discharge hole for ozone water in the inner cylinder is formed at a lower end of the inner cylinder in contact with the bottom of the inner cylinder.

【0007】なお、前記オゾン水タンクの底部には、上
記内筒の外側を囲むように突縁を形成するのが好まし
い。
Preferably, a projecting edge is formed at the bottom of the ozone water tank so as to surround the outside of the inner cylinder.

【0008】また、前記オゾン水タンクの吐出口を、前
記渦の巻き方向に沿って形成するように構成するのが望
ましい。
It is desirable that the discharge port of the ozone water tank is formed along the spiral direction of the vortex.

【0009】さらに、前記内筒の下端を逆円錐状の底蓋
で閉じるとともに、前記オゾン水の排出孔を上記底蓋の
上端縁に形成するのが好ましい。
Further, it is preferable that the lower end of the inner cylinder is closed by an inverted conical bottom lid, and the ozone water discharge hole is formed at the upper end edge of the bottom lid.

【0010】加えて、前記気液混合水の流入口を前記内
筒の上部に形成することに代えて内筒の下部に形成する
とともに、内筒内のオゾン水を排出する排出孔を、前記
内筒の下部に形成することに代えて内筒の上部に形成す
るようにしてもよい。
In addition, instead of forming the inflow port of the gas-liquid mixed water at the upper part of the inner cylinder, it is formed at the lower part of the inner cylinder, and the discharge hole for discharging the ozone water in the inner cylinder is formed. Instead of being formed at the lower part of the inner cylinder, it may be formed at the upper part of the inner cylinder.

【0011】[0011]

【発明の実施の形態】図1は本発明に係るオゾン水生成
器の概要図である。このオゾン水生成器本体1は公知の
オゾン水生成器と同じ構造を有するもので、オゾン発生
体(オゾナイザー)1と、水道蛇口2からの給水管3の
途中に配置したエジェクタ4と、エジェクタ4に水道水
を通す際にオゾンを吸引させて水道水にオゾンガスを混
合、溶解させた後に、オゾン水から余剰オゾンガスを分
離するためのオゾン水タンク5と、分離されたオゾンガ
スを処理する処理装置6と、排出ホース7とから構成さ
れている。オゾン発生体1で発生したオゾンガスはエジ
ェクタ4に吸引されて水道水と混じり合い、オゾン水タ
ンク5に貯留された後、このタンク5内に設けられた気
液分離装置によりオゾンガスは処理装置6で分解処理さ
れて大気に排出され、オゾン水は排出ホース7により排
出されて使用に供される。
FIG. 1 is a schematic diagram of an ozone water generator according to the present invention. The ozone water generator main body 1 has the same structure as a known ozone water generator, and includes an ozone generator (ozonizer) 1, an ejector 4 arranged in the middle of a water supply pipe 3 from a water tap 2, and an ejector 4. The ozone water tank 5 for separating the excess ozone gas from the ozone water after mixing and dissolving the ozone gas in the tap water by sucking ozone when passing the tap water through the water, and the processing device 6 for processing the separated ozone gas And a discharge hose 7. The ozone gas generated by the ozone generator 1 is sucked by the ejector 4, mixed with the tap water and stored in the ozone water tank 5. It is decomposed and discharged to the atmosphere, and the ozone water is discharged by a discharge hose 7 and used for use.

【0012】上記気液分離装置は、図2に示されるよう
に、オゾン水タンク5の内側(中央でなくてもよい)
に、上端を上蓋11で閉じた内筒10を配置し、内筒1
0の上部の流入口8に給水管3を開口させ、内筒10の
上蓋11にはオゾンガスの排気孔13を形成し、内筒1
0の下端にはオゾン水の排出孔14を形成するととも
に、オゾン水タンク5の下部には吐出口9を形成したも
のである。内筒10の下端はオゾン水タンク5の底部に
当接している。給水管3は図3に示されるように内筒1
0の中心から偏心した位置に配置されている。このた
め、流入口8から流入した気液混合水の水流は、内筒1
0の内部で渦を巻くように流れる。
As shown in FIG. 2, the gas-liquid separator is located inside the ozone water tank 5 (not necessarily at the center).
, An inner cylinder 10 whose upper end is closed by an upper lid 11 is disposed.
The water supply pipe 3 is opened at the inflow port 8 at the upper part of the inner cylinder 10, and an ozone gas exhaust hole 13 is formed at the upper lid 11 of the inner cylinder 10.
An ozone water discharge hole 14 is formed at the lower end of the nozzle 0, and a discharge port 9 is formed at the lower part of the ozone water tank 5. The lower end of the inner cylinder 10 is in contact with the bottom of the ozone water tank 5. The water supply pipe 3 is, as shown in FIG.
It is arranged at a position eccentric from the center of 0. For this reason, the water flow of the gas-liquid mixed water flowing from the inlet 8 is
It flows like a swirl inside zero.

【0013】処理装置6内には通常は触媒が充填され、
オゾンガスは触媒内を移動するうちに分解され、大気に
排出される。
The processing unit 6 is usually filled with a catalyst,
Ozone gas is decomposed while moving through the catalyst and is discharged to the atmosphere.

【0014】上記構成によれば、オゾン発生体1で発生
したオゾンガスはエジェクタ4に吸引されて水道水と混
じり合い、流入口8から給水管3を経てオゾン水タンク
5の内筒10に流入する。流入した気液混合水は内筒1
0の内面の接線方向に流れ込んだ後、遠心力によってそ
の外周面に沿って渦巻き状に回り込みながら下方に延
び、さらに下端の排出孔14から内筒10の外側に排出
されて貯留され、さらに吐出口9から排出ホース7によ
って排出される。
According to the above configuration, the ozone gas generated by the ozone generator 1 is sucked by the ejector 4 and mixed with the tap water, and flows into the inner tube 10 of the ozone water tank 5 from the inflow port 8 through the water supply pipe 3. . The gas-liquid mixed water that has flowed into the inner cylinder 1
After flowing in the tangential direction of the inner surface of the inner cylinder 10, it extends downward while spiraling around the outer peripheral surface due to centrifugal force, and is further discharged from the lower end discharge hole 14 to the outside of the inner cylinder 10 and stored there. It is discharged from the outlet 9 by the discharge hose 7.

【0015】ところで、気液混合水が渦を巻くことで延
伸力による分離作用が働き、質量の小さいオゾンガスの
気泡aは渦の中央側に集まる。また、中央に集まったオ
ゾンガスは浮力によりオゾン水の上方に浮上して排気孔
13から排出されて処理装置6に運ばれる。オゾンガス
は処理装置6で分解処理されて大気に排出される。
By the way, the gas-liquid mixed water swirls to cause a separating action by the stretching force, and the bubbles a of the ozone gas having a small mass are collected at the center of the swirl. Further, the ozone gas collected at the center floats above the ozone water by buoyancy, is discharged from the exhaust holes 13, and is carried to the processing device 6. The ozone gas is decomposed by the processing device 6 and discharged to the atmosphere.

【0016】また、内筒10内の渦は断面が逆三角形状
になり、渦の内側に引き込まれたオゾンガスの気泡aは
オゾン水の排出孔14からは遠くに位置する。このた
め、オゾン水の排出孔14から外に出ることはほとんど
できない。
The cross section of the vortex in the inner cylinder 10 has an inverted triangular shape, and the bubble a of the ozone gas drawn inside the vortex is located far from the ozone water discharge hole 14. For this reason, it is hardly possible to go out of the ozone water discharge hole 14.

【0017】さらに、オゾン水の渦巻き流は内筒10の
中の小さな範囲内で起こるが、渦は小さい方が気液の分
離性能がよい。
Furthermore, the swirling flow of the ozone water occurs within a small area in the inner cylinder 10, and the smaller the vortex, the better the gas-liquid separation performance.

【0018】なお、好ましくは流入口8の口径をR1、
オゾンガスの排気孔13の孔径をR2、オゾン水の排出
孔14の孔径R3とすると、R1はR3と同じかそれよ
りも大きく、R3はR2よりもかなり大きく形成するの
が好ましい。これによって内筒10の内圧が高まり、渦
の巻き状態がよく、気液の分離能力が良くなる。
Preferably, the diameter of the inlet 8 is R1,
Assuming that the hole diameter of the ozone gas exhaust hole 13 is R2 and the hole diameter of the ozone water discharge hole 14 is R3, it is preferable that R1 be equal to or larger than R3, and that R3 be considerably larger than R2. As a result, the internal pressure of the inner cylinder 10 increases, the spiral state is improved, and the gas-liquid separation ability is improved.

【0019】上述のように、オゾン水とそれに含まれる
オゾンガスの気泡aは内筒10の中で確実に分離される
ので、オゾン水タンク5の高さをあまり高くする必要が
なく、コンパクトにすることができる。
As described above, since the ozone water and the bubbles a of the ozone gas contained therein are reliably separated in the inner cylinder 10, the height of the ozone water tank 5 does not need to be too high, and the ozone water tank 5 is made compact. be able to.

【0020】ところで、図4は内筒10をオゾン水タン
ク5の一側に寄せて配置し、オゾン水タンク5の底部に
は、上記内筒10の外側を囲むように突縁15を形成し
た例である。
In FIG. 4, the inner cylinder 10 is disposed so as to be close to one side of the ozone water tank 5, and a projecting edge 15 is formed at the bottom of the ozone water tank 5 so as to surround the outside of the inner cylinder 10. It is an example.

【0021】この構成によれば、万一気泡aが内筒10
のオゾン水排出孔14から出たとしても、図5に示すよ
うに、気泡aは吐出口9側に流れ込む前に突縁15を越
えて上昇する。この上昇時に浮力がついて気泡aは上昇
する。したがって、突縁15の高さは高い方が好まし
い。
According to this configuration, the bubble a should be
5, the bubble a rises beyond the protruding edge 15 before flowing into the discharge port 9 side as shown in FIG. At the time of this rise, buoyancy is applied and the bubble a rises. Therefore, the height of the protruding edge 15 is preferably higher.

【0022】なお、内筒10をオゾン水タンク5の中央
側に配置し、そのまわりに円形状の突縁15を巡らせる
構成であってもよい。
The inner cylinder 10 may be arranged at the center of the ozone water tank 5, and a circular protruding edge 15 may be wrapped therearound.

【0023】次に、図6はオゾン水タンク5の吐出口9
を、渦の巻き方向に沿って形成した例である。
Next, FIG. 6 shows the discharge port 9 of the ozone water tank 5.
Are formed along the spiral direction.

【0024】これによれば、内筒10の排出孔14から
排出されたオゾン水は同じ巻き方向に回りながら吐出口
9に流れ込む。このように、内筒10の内側と外側とに
同じ巻き方向の渦ができるので、遠心力が高まり、気泡
aが内筒10の排気孔13から排出されたとき、図7の
ように遠心力の作用により内筒10の外面に気泡aが集
まり、集まった気泡aは大きくなって浮力が増し、上昇
する。したがって、気液は良好に分離する。
According to this, the ozone water discharged from the discharge hole 14 of the inner cylinder 10 flows into the discharge port 9 while rotating in the same winding direction. As described above, the vortex having the same winding direction is formed on the inner side and the outer side of the inner cylinder 10, thereby increasing the centrifugal force. When the bubble “a” is discharged from the exhaust hole 13 of the inner cylinder 10, as shown in FIG. As a result, the bubbles a collect on the outer surface of the inner cylinder 10, and the collected bubbles a become larger, the buoyancy increases, and the bubbles a rise. Therefore, gas-liquid is well separated.

【0025】また、図8は、内筒10の下端を逆円錐状
の底蓋16で閉じるとともに、オゾン水の排出孔14を
上記底蓋16の上端縁に形成した例である。
FIG. 8 shows an example in which the lower end of the inner cylinder 10 is closed by an inverted conical bottom lid 16 and the ozone water discharge hole 14 is formed on the upper edge of the bottom lid 16.

【0026】この構成によれば、気液混合水は内筒10
内に渦を作り、下方に延びてくるが、底部は逆円錐状に
なっているため、遠心力が高まるが、同時に圧力も高く
なる。このため、渦は下方に延びることはできず、内筒
10の上部に形成される。オゾンガスの気泡は渦の内側
に引き込まれるから、気泡aも内筒10の上部に集まる
ということになる。したがって、上記排出孔14からは
オゾン水のみが排出されるから、気液の分離能力が向上
する。
According to this configuration, the gas-liquid mixed water is supplied to the inner cylinder 10
It creates a vortex inside and extends downward, but the bottom is in the shape of an inverted cone, which increases the centrifugal force but also increases the pressure. For this reason, the vortex cannot extend downward, but is formed at the upper part of the inner cylinder 10. Since the ozone gas bubbles are drawn into the inside of the vortex, the bubbles a also collect at the upper part of the inner cylinder 10. Therefore, only the ozone water is discharged from the discharge hole 14, so that the gas-liquid separation ability is improved.

【0027】次に、図9は、気液混合水の流入口8を内
筒10の下部に形成するとともに、内筒10内のオゾン
水を排出する排出孔14を内筒10の上部に形成した例
である。
Next, FIG. 9 shows that the inlet 8 for the gas-liquid mixed water is formed in the lower part of the inner cylinder 10 and the discharge hole 14 for discharging the ozone water in the inner cylinder 10 is formed in the upper part of the inner cylinder 10. This is an example.

【0028】この構成によれば、流入口8から流入した
気液混合水は上方に渦を巻きながら移動していくが、混
合水中のオゾンガスの気泡aも上方に移動する。そし
て、オゾン水はやがて内筒10の上部の排出孔14から
外に排出される。排出されたオゾン水の中に気泡aが混
入していても、気泡aはその浮力によってオゾン水の水
面から空中に飛散するから吐出口9にはオゾン水のみが
流れ込む。また、内筒10中の気泡aは排気孔13、1
3aから排出される。したがって、気液は良好に分離さ
れる。
According to this configuration, the gas-liquid mixed water flowing from the inflow port 8 moves upward while swirling, and the bubbles a of the ozone gas in the mixed water also move upward. Then, the ozone water is discharged to the outside through the discharge hole 14 on the upper part of the inner cylinder 10. Even if air bubbles a are mixed in the discharged ozone water, the air bubbles a scatter from the surface of the ozone water into the air due to their buoyancy, so that only the ozone water flows into the discharge port 9. Also, the bubbles a in the inner cylinder 10 are exhaust holes 13, 1
It is discharged from 3a. Therefore, gas-liquid is well separated.

【図面の簡単な説明】[Brief description of the drawings]

【図1】オゾン水生成器の概略図FIG. 1 is a schematic diagram of an ozone water generator.

【図2】本発明に係るオゾン水生成器における気液分離
装置の一例の縦断面図
FIG. 2 is a longitudinal sectional view of an example of a gas-liquid separation device in the ozone water generator according to the present invention.

【図3】上記気液分離装置の平面図FIG. 3 is a plan view of the gas-liquid separation device.

【図4】上記気液分離装置の他の例の縦断面図FIG. 4 is a longitudinal sectional view of another example of the gas-liquid separation device.

【図5】上記気液分離装置の要部の縦断面図FIG. 5 is a longitudinal sectional view of a main part of the gas-liquid separation device.

【図6】上記気液分離装置のさらに他の例の横断面図FIG. 6 is a cross-sectional view of still another example of the gas-liquid separation device.

【図7】上記気液分離装置の要部の縦断面図FIG. 7 is a longitudinal sectional view of a main part of the gas-liquid separation device.

【図8】上記気液分離装置の別の例の縦断面図FIG. 8 is a longitudinal sectional view of another example of the gas-liquid separation device.

【図9】上記気液分離装置のさらに別の例の縦断面図FIG. 9 is a longitudinal sectional view of still another example of the gas-liquid separation device.

【図10】従来の気液分離装置の要部の模式図FIG. 10 is a schematic view of a main part of a conventional gas-liquid separation device.

【符号の説明】[Explanation of symbols]

1 オゾン水生成器 5 オゾン水タンク 8 流入口 9 吐出口 10 内筒 11 上蓋 13、14 排出孔 DESCRIPTION OF SYMBOLS 1 Ozone water generator 5 Ozone water tank 8 Inflow port 9 Discharge port 10 Inner cylinder 11 Top lid 13, 14 Discharge hole

───────────────────────────────────────────────────── フロントページの続き (72)発明者 藤井 清人 東京都中央区日本橋箱崎町6番6号 マッ クス株式会社内 (72)発明者 戸花 直樹 東京都中央区日本橋箱崎町6番6号 マッ クス株式会社内 (72)発明者 坂田 知昭 東京都中央区日本橋箱崎町6番6号 マッ クス株式会社内 Fターム(参考) 4D011 AA05 AC04 AC06 AD03 4D037 AA02 AB03 BA04 BB03 BB04 4G035 AA02 AB20 AC44 4G042 CE01  ──────────────────────────────────────────────────の Continued on the front page (72) Inventor Kiyoto Fujii 6-6 Nihonbashi-Hakozakicho, Chuo-ku, Tokyo Inside Max Corporation (72) Inventor Naoki Tohana 6-6 Nihonbashi-Hakozakicho, Chuo-ku, Tokyo Max Co., Ltd. (72) Inventor Tomoaki Sakata 6-6, Hakozakicho, Nihonbashi, Chuo-ku, Tokyo F-term (reference) 4D011 AA05 AC04 AC06 AD03 4D037 AA02 AB03 BA04 BB03 BB04 4G035 AA02 AB20 AC44 4G042 CE01

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 オゾン発生体で発生させたオゾンガスを
水に溶かした状態で貯留するオゾン水タンクを備えたオ
ゾン水生成器において、 上記オゾン水タンクの上部には水とオゾンガスの気液混
合水の流入口を、下部には吐出口を形成するとともに、
オゾン水タンクの内側に上端を上蓋で閉じた内筒を配置
し、 上記流入口から内筒の上部に気液混合水が渦を巻いて流
入するようになし、内筒の上蓋にはオゾンガスの排気孔
を形成するとともに、外筒の底部に当接した内筒の下端
には内筒内のオゾン水の排出孔を形成したことを特徴と
するオゾン水生成器における気液分離装置。
1. An ozone water generator comprising an ozone water tank for storing ozone gas generated by an ozone generator in a state of being dissolved in water, wherein a gas-liquid mixture of water and ozone gas is provided above the ozone water tank. And an outlet at the bottom,
An inner cylinder whose upper end is closed with an upper lid is placed inside the ozone water tank, and the gas-liquid mixed water is swirled into the upper part of the inner cylinder from the inflow port. A gas-liquid separator in an ozone water generator, wherein an exhaust hole is formed, and a discharge hole of ozone water in the inner cylinder is formed at a lower end of the inner cylinder in contact with a bottom of the outer cylinder.
【請求項2】 前記オゾン水タンクの底部には、上記内
筒の外側を囲むように突縁を形成した、請求項1記載の
オゾン水生成器における気液分離装置。
2. The gas-liquid separation device in the ozone water generator according to claim 1, wherein a protruding edge is formed at a bottom portion of the ozone water tank so as to surround an outside of the inner cylinder.
【請求項3】 前記オゾン水タンクの吐出口を、前記渦
の巻き方向に沿って形成した、請求項1記載のオゾン水
生成器における気液分離装置。
3. The gas-liquid separator in the ozone water generator according to claim 1, wherein a discharge port of the ozone water tank is formed along a spiral direction of the vortex.
【請求項4】 前記内筒の下端を逆円錐状の底蓋で閉じ
るとともに、前記オゾン水の排出孔を上記底蓋の上端縁
に形成した、請求項1記載のオゾン水生成器における気
液分離装置。
4. The gas-liquid in the ozone water generator according to claim 1, wherein a lower end of the inner cylinder is closed by an inverted conical bottom cover, and a discharge hole of the ozone water is formed at an upper end edge of the bottom cover. Separation device.
【請求項5】 前記気液混合水の流入口を前記内筒の上
部に形成することに代えて内筒の下部に形成するととも
に、内筒内のオゾン水を排出する排出孔を、前記内筒の
下部に形成することに代えて内筒の上部に形成した、請
求項1記載のオゾン水生成器における気液分離装置。
5. The gas-liquid mixed water inflow port is formed at a lower portion of the inner cylinder instead of at an upper portion of the inner cylinder, and a discharge hole for discharging ozone water in the inner cylinder is formed in the inner cylinder. The gas-liquid separation device for an ozone water generator according to claim 1, wherein the gas-liquid separator is formed at an upper part of the inner cylinder instead of at a lower part of the cylinder.
JP2000217887A 2000-07-18 2000-07-18 Gas-liquid separator in ozone water producer Pending JP2002028635A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000217887A JP2002028635A (en) 2000-07-18 2000-07-18 Gas-liquid separator in ozone water producer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000217887A JP2002028635A (en) 2000-07-18 2000-07-18 Gas-liquid separator in ozone water producer

Publications (1)

Publication Number Publication Date
JP2002028635A true JP2002028635A (en) 2002-01-29

Family

ID=18712932

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2002028635A (en)

Cited By (10)

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JP2005000882A (en) * 2003-06-13 2005-01-06 Aura Tec:Kk Apparatus for generating micro bubble
JP2011088061A (en) * 2009-10-22 2011-05-06 Japan Organo Co Ltd Gas-liquid dissolving tank
JP2011104501A (en) * 2009-11-16 2011-06-02 Mingasu:Kk Gas separation apparatus and gas separation method
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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005000882A (en) * 2003-06-13 2005-01-06 Aura Tec:Kk Apparatus for generating micro bubble
JP2011088061A (en) * 2009-10-22 2011-05-06 Japan Organo Co Ltd Gas-liquid dissolving tank
JP2011104501A (en) * 2009-11-16 2011-06-02 Mingasu:Kk Gas separation apparatus and gas separation method
KR101157168B1 (en) * 2011-07-04 2012-06-20 동양특수콘크리트 (주) Bubble rremoving apparatus for watet
JP2013081880A (en) * 2011-10-06 2013-05-09 Clean Tech Service:Kk Gas dissolving apparatus
WO2013088961A1 (en) * 2011-12-14 2013-06-20 シャープ株式会社 Gas-liquid separator, ozone water device provided with same, and washing apparatus for sanitary fitting provided with same
JP2013123674A (en) * 2011-12-14 2013-06-24 Sharp Corp Gas-liquid separator, ozone water generator with the same, and washing apparatus for sanitary fitting with the same
JP2013154284A (en) * 2012-01-27 2013-08-15 Sharp Corp Gas-liquid separator, solution generation device with the same and sanitary equipment cleaning device equipped with the same
JP2013240782A (en) * 2012-04-27 2013-12-05 Shinichi Watabe Oil excepter
WO2019163105A1 (en) * 2018-02-23 2019-08-29 エコデザイン株式会社 Ozone solution generation apparatus and ozone solution generation method
JPWO2019163105A1 (en) * 2018-02-23 2020-12-17 エコデザイン株式会社 Ozone solution generator and ozone solution generation method
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